US1442520A - Purification of isopropyl ether - Google Patents
Purification of isopropyl ether Download PDFInfo
- Publication number
- US1442520A US1442520A US510637A US51063721A US1442520A US 1442520 A US1442520 A US 1442520A US 510637 A US510637 A US 510637A US 51063721 A US51063721 A US 51063721A US 1442520 A US1442520 A US 1442520A
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- US
- United States
- Prior art keywords
- ether
- sulfuric acid
- purification
- crude
- water
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
- C07C41/01—Preparation of ethers
- C07C41/34—Separation; Purification; Stabilisation; Use of additives
- C07C41/36—Separation; Purification; Stabilisation; Use of additives by solid-liquid treatment; by chemisorption
Definitions
- UNHT ares taiasaa PATENT HYYM E. BUC, OF ROSELLE, NEW JERSEY, ASSIGNOR, BY MESNE ASSIGNMENTS, T0 STANDARD DEVELOPMENT COMPANY, A CORPORATION OF. DELAWARE.
- the present invention relates to the purification of isopropyl ether, and more partlcularly to the purification of crude ether obtained, for example, by the treatment of isopropyl alcohol with sulfuric acid under the proper conditions of concentration and temperature.
- the crude ether subjected to treatment in accordance with the present process may have associated with it small quantities of isopropyl alcohol, propylene and polymerized hydrocarbons, as well as compounds, the character of which is as yet unknown, which cause a marked discolora tion of the crude material and impart to it foreign, disagreeable odors.
- the crude isopropyl ether is subjected to the action of diluted sulfuric acid of a concentration between 65 and 80% H SO 75% sulfuric acid is preferred, as it appears to give the best results in practice.
- the ether dissolves in the sulfuric acid almost instantaneously, with evolution of heat.
- The'proportion of sulfuric acid may be varied greatly and the sulfuric acid used may be added as a whole or in fractional portions.
- the total volume of sulfuric acid employed thus may be from g the volume of crude ether upwards.
- the solution of ether in sulfuric acid is preferably decanted before the addition of the next portion of sulfuric acid.
- the ethersolutions are mixed after their withdrawal.
- the sulfuric acid solution of the ether may then be diluted with water until the greater portion of the ether is thrown out as a supernatant layer. This stage is readily recognizable by the appearance of the mixture and by the fact that on further addition of water, the volume of the ether does not in- Application filed October 26, 1921. Serial No. 510,637.
- the separated ether may then be dried in any suitable manner; for example, by the addition of quick lime or calcium chloride and distillation of the dehydrated ether.
- the acid layer which separates on dilution of the sulfuric acid solution of ether with water contains a small proportion of the ether, as the ether is soluble to the extent of f or 5% in water. This solution may be fractionally distilled to separate the dissolved ether, which may then be dehydrated and.
- the crude ether may be sub.- jected to washing with water prior to its treatment with sulfuric acid. This washing with water Will remove any water-soluble impurities contained in the crude ether, as for example, isopropyl alcohol. Any ether dis solved in the wash water may be separated by fractional distillation and, if desired, added to the ether undergoing purification.
- the purified isopropyl ether obtained in accordance with the present invention is a colorless liquid having a boiling point of 68.2 to 68.7 C.
Description
Patented date Re, 11923.
UNHT ares taiasaa PATENT HYYM E. BUC, OF ROSELLE, NEW JERSEY, ASSIGNOR, BY MESNE ASSIGNMENTS, T0 STANDARD DEVELOPMENT COMPANY, A CORPORATION OF. DELAWARE.
PURIFICATION OF ISOPROPYL ETHER.
N 0 Drawing.
To all 1072077? it may concern Be it known that I, HYYM E. BUG, a citizen of the United States, residing at 620 Locust Street, Roselle, in the count-y of Union and State of New Jersey, have invented a new and useful Improvement in the Purification of I'sopropyl Ether, of wh1ch the following is a specification.
The present invention relates to the purification of isopropyl ether, and more partlcularly to the purification of crude ether obtained, for example, by the treatment of isopropyl alcohol with sulfuric acid under the proper conditions of concentration and temperature. The crude ether subjected to treatment in accordance with the present process may have associated with it small quantities of isopropyl alcohol, propylene and polymerized hydrocarbons, as well as compounds, the character of which is as yet unknown, which cause a marked discolora tion of the crude material and impart to it foreign, disagreeable odors.
In accordance with the present invention, the crude isopropyl ether is subjected to the action of diluted sulfuric acid of a concentration between 65 and 80% H SO 75% sulfuric acid is preferred, as it appears to give the best results in practice. The ether dissolves in the sulfuric acid almost instantaneously, with evolution of heat. The'proportion of sulfuric acid may be varied greatly and the sulfuric acid used may be added as a whole or in fractional portions. The total volume of sulfuric acid employed thus may be from g the volume of crude ether upwards. In practice it is preferred to add the diluted sulfuric acid to the crude ether in portions eachhaving about onehalf the volume of the original crude ether and continuing this until the addition of the acid causes no further substantial rise in temperature. The solution of ether in sulfuric acid is preferably decanted before the addition of the next portion of sulfuric acid. The ethersolutions are mixed after their withdrawal.
The sulfuric acid solution of the ether may then be diluted with water until the greater portion of the ether is thrown out as a supernatant layer. This stage is readily recognizable by the appearance of the mixture and by the fact that on further addition of water, the volume of the ether does not in- Application filed October 26, 1921. Serial No. 510,637.
crease. In general, it is found sufficient to dilute the solution of ether in sulfuric acid until the separated acid layer has a strength of about 25% sulfuric acid.
The separated ether may then be dried in any suitable manner; for example, by the addition of quick lime or calcium chloride and distillation of the dehydrated ether. The acid layer which separates on dilution of the sulfuric acid solution of ether with water contains a small proportion of the ether, as the ether is soluble to the extent of f or 5% in water. This solution may be fractionally distilled to separate the dissolved ether, which may then be dehydrated and.
distilled in the manner described above and may be added to the purified ether or to a fresh batch of ether subjected to the purifying operation. i
. If desired, the crude ether may be sub.- jected to washing with water prior to its treatment with sulfuric acid. This washing with water Will remove any water-soluble impurities contained in the crude ether, as for example, isopropyl alcohol. Any ether dis solved in the wash water may be separated by fractional distillation and, if desired, added to the ether undergoing purification.
t. The purified isopropyl ether obtained in accordance with the present invention is a colorless liquid having a boiling point of 68.2 to 68.7 C.
I claim:
1. The method of purifying isopropyl other which comprises admixing the ether with sulfuric acid of a strength between 65 and 80%, diluting the resultant solution of the ether in the acid, thereby separating the ether. I
2. The method of purifying isopropyl ether which comprises admixin the ether with sulfuric acid of a strengt of about 75%, diluting the resultant solution of the 5 ether which comprises admixing the crude 'ether with successive portions of 75% sulfuric acid, the volume of each of said por tions being about one-half that of the crude ether, until solution of the ether in the sulfuric acid is substantially complete, adding water to the solution of ether in sulfuric acid until the ether separates therefrom, and removing the separated ether.
" 5.. The method of purifying isopropyl ether which comprises admixlng the ether with sulfuric acid ofa strength between 60 and 85%, diluting the resulting solution of ether in the acid with water thereby separating out the ether, removing and dehydrating the separated ether.
6. The method of purifying isopropyl ether which comprises washin the crude ether with water, then admixing it with sulfuric acid with a strength between 60 and 85%, thereby dissolving the ether, adding water to the resulting solution of ether to separate out the ether and removing the separated ether.
HYYM' E. BUG.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US510637A US1442520A (en) | 1921-10-26 | 1921-10-26 | Purification of isopropyl ether |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US510637A US1442520A (en) | 1921-10-26 | 1921-10-26 | Purification of isopropyl ether |
Publications (1)
Publication Number | Publication Date |
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US1442520A true US1442520A (en) | 1923-01-16 |
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Application Number | Title | Priority Date | Filing Date |
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US510637A Expired - Lifetime US1442520A (en) | 1921-10-26 | 1921-10-26 | Purification of isopropyl ether |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2446408A (en) * | 1946-02-25 | 1948-08-03 | Gen Electric | Preparation of anhydrous ether |
US4262149A (en) * | 1980-04-21 | 1981-04-14 | Columbian Chemicals Company | Process for separating alkanols from aqueous calcium chloride |
US4322565A (en) * | 1979-08-23 | 1982-03-30 | Columbian Chemicals Company | Process for purifying ethers |
US4459178A (en) * | 1983-04-25 | 1984-07-10 | Lloyd Berg | Separation of isopropyl ether from methyl ethyl ketone by extractive distillation |
US4459179A (en) * | 1983-01-06 | 1984-07-10 | Lloyd Berg | Separation of isopropyl ether from acetone by extractive distillation |
US4469491A (en) * | 1982-04-19 | 1984-09-04 | Sun Tech, Inc. | Separation of diisopropylether from hydrocarbon streams |
US4666563A (en) * | 1985-11-20 | 1987-05-19 | Lloyd Berg | Separation of isopropyl ether from isopropanol and water by extractive distillation |
US20070244330A1 (en) * | 2005-04-21 | 2007-10-18 | Reardan Dayton T | Ultrapure 4-methylpyrazole |
-
1921
- 1921-10-26 US US510637A patent/US1442520A/en not_active Expired - Lifetime
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2446408A (en) * | 1946-02-25 | 1948-08-03 | Gen Electric | Preparation of anhydrous ether |
US4322565A (en) * | 1979-08-23 | 1982-03-30 | Columbian Chemicals Company | Process for purifying ethers |
US4262149A (en) * | 1980-04-21 | 1981-04-14 | Columbian Chemicals Company | Process for separating alkanols from aqueous calcium chloride |
US4469491A (en) * | 1982-04-19 | 1984-09-04 | Sun Tech, Inc. | Separation of diisopropylether from hydrocarbon streams |
US4459179A (en) * | 1983-01-06 | 1984-07-10 | Lloyd Berg | Separation of isopropyl ether from acetone by extractive distillation |
US4459178A (en) * | 1983-04-25 | 1984-07-10 | Lloyd Berg | Separation of isopropyl ether from methyl ethyl ketone by extractive distillation |
US4666563A (en) * | 1985-11-20 | 1987-05-19 | Lloyd Berg | Separation of isopropyl ether from isopropanol and water by extractive distillation |
US20070244330A1 (en) * | 2005-04-21 | 2007-10-18 | Reardan Dayton T | Ultrapure 4-methylpyrazole |
US7553863B2 (en) | 2005-04-21 | 2009-06-30 | Paladin Labs (Barbados) Inc. | Ultrapure 4-methylpyrazole |
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